An apparatus for producing o-tert-butylphenol and a method of use

Abstract

The application discloses a production device and method of o-t-butyl phenol, relates to the o-t-butyl phenol production technical field, and has the advantages that the isobutene gas floating in the reaction kettle is allowed to participate in the reaction again, and the technical scheme points are as follows: the device comprises a reaction kettle, a disc, and a gas inlet pipe and a hot water pipeline arranged above one side of the outer wall of the reaction kettle, a dispersion pipe is horizontally arranged below the reaction kettle between opposite sides, a plurality of spray heads are arranged on the outer wall of the dispersion pipe, the gas inlet pipe is communicated with the dispersion pipe, the disc is rotationally connected to one side in the reaction kettle, a plurality of connecting plates are horizontally arranged on one side of the disc, the connecting plates are uniformly distributed along the axis of the disc, a groove for bringing the isobutene gas into the reaction liquid in the reaction kettle is arranged on one side of each connecting plate along the length direction of the connecting plate, a driving member for driving the disc to rotate is arranged on the reaction kettle, a feeding pipe is arranged at the top end of the reaction kettle, and a discharging pipe with a valve is arranged at the bottom end of the reaction kettle.

Description

TECHNICAL FIELD

[0001] The present application relates to the technical field of o-tert-butyl phenol production, in particular to a production device and use method of o-tert-butyl phenol. BACKGROUND

[0002] The o-tert-butyl phenol generally refers to 2-tert-butyl phenol. The product is mainly used as an antioxidant, a plant protection agent, a synthetic resin, a medicine, a pesticide intermediate and a raw material of a flavoring agent.

[0003] In the prior art, the o-tert-butyl phenol is prepared by adding phenol, concentrated sulfuric acid and anhydrous aluminum chloride into a reaction kettle, heating to 50 DEG C, and introducing isobutene gas into the reaction liquid in the reaction kettle by using an isobutene gas inlet pipe under the condition of vigorous stirring, then adding hot water into the reaction kettle through a hot water pipeline after the reaction is completed, and then performing hydrolysis after sufficient stirring, and then entering a hydrolysis kettle, and then entering a filter, and then entering a first rectifying tower and a second rectifying tower in sequence for rectification to obtain the o-tert-butyl phenol product.

[0004] However, when the isobutene gas is introduced into the reaction liquid in the reaction kettle for reaction, the isobutene gas overflowing from the reaction liquid floats in the reaction kettle, and the utilization rate of the isobutene gas is low. Therefore, the present applicant has developed a new technical solution in the actual production process to solve the above technical problems. SUMMARY

[0005] The present application aims to provide a production device and use method of o-tert-butyl phenol, which has the advantage that the isobutene gas floating in the reaction kettle is involved in the reaction again.

[0006] To solve the above technical problems, the present application adopts the following technical solution:

[0007] The present application provides a production device of o-tert-butyl phenol, which comprises a reaction kettle, a disc and a gas inlet pipe and a hot water pipeline arranged on the upper side of one side of the outer wall of the reaction kettle, a dispersion pipe arranged horizontally below the reaction kettle between the opposite sides of the reaction kettle, a plurality of nozzles arranged on the outer wall of the dispersion pipe, the gas inlet pipe being communicated with the dispersion pipe, the disc being rotationally connected to one side in the reaction kettle, a plurality of connecting plates being arranged horizontally on one side of the disc and being uniformly distributed along the circumference of the disc, a groove for bringing the isobutene gas into the reaction liquid in the reaction kettle being arranged on one side of each connecting plate along the length direction of the connecting plate, a driving member for driving the disc to rotate being arranged on the top end of the reaction kettle, a feeding pipe being arranged on the top end of the reaction kettle, and a discharging pipe with a valve being arranged on the bottom end of the reaction kettle.

[0008] By adopting the technical scheme, the water level of the reaction liquid in the reaction kettle is located at the upper middle side of the disc, in use, the isobutene gas is introduced into the dispersion pipe through the gas inlet pipe, and the disc is driven to rotate by the driving member, at this time, the isobutene gas is sprayed into the reaction liquid in the reaction kettle through the nozzles on the dispersion pipe to react, when the disc rotates, the disc drives each connecting plate to rotate along the rotation axis of the disc, at this time, because the water level of the reaction liquid is located at the upper middle side of the disc, part of the connecting plates on the disc is located outside the reaction liquid, and the remaining connecting plates are located in the reaction liquid, when the disc drives each connecting plate to rotate along the rotation axis of the disc, the side of the connecting plate provided with the groove located outside the reaction liquid is first contacted with the reaction liquid with the rotation of the disc, and then the connecting plate rotates into the reaction liquid with the rotation of the disc, at this time, when the isobutene gas overflows from the reaction liquid and floats in the reaction kettle, the isobutene gas floating in the reaction kettle can be brought into the reaction liquid again to participate in the reaction through the groove on the connecting plate located outside the reaction liquid and rotating with the disc, and the reaction liquid in the reaction kettle can be stirred through each connecting plate on the disc.

[0009] After the reaction is completed, hot water is added into the reaction kettle through the hot water pipeline, the reaction liquid is stirred, the valve on the discharge pipe is opened, and the reaction liquid can be discharged through the discharge pipe, which is simple and convenient to use.

[0010] Preferably, the driving member comprises an inner gear ring and a circular groove coaxially arranged on the disc, the inner gear ring is coaxially located in the circular groove, and the outer wall of the inner gear ring is fixedly connected with the groove wall of the circular groove, one end of the rotating shaft of the motor is provided with a gear and penetrates through the wall of the reaction kettle, and the gear is located in the inner gear ring and is engaged with the inner gear ring.

[0011] Preferably, the inner wall of the reaction kettle is rotatably connected with a supporting ring opposite to the disc, and one end of each connecting plate away from the disc is fixedly connected with the supporting ring.

[0012] Preferably, the reaction kettle is provided with a stirring member for stirring the reaction liquid in the reaction kettle, and the gear is used to drive the stirring member to stir the reaction liquid in the reaction kettle when the gear rotates.

[0013] Preferably, the stirring member comprises a stirring shaft rotatably connected to one side of the inner wall of the reaction kettle, the stirring shaft is horizontally arranged and opposite to the gear, one end of the stirring shaft is located in the supporting ring at this time, and the other end of the stirring shaft is fixedly connected with the gear in a coaxial manner, and a plurality of stirring rods are arranged on the stirring shaft.

[0014] Preferably, the dispersion pipe is located below the disc and the supporting ring, and the dispersion pipe is parallel to the stirring shaft.

[0015] Preferably, the opposite sides of the inner wall of the reaction kettle are vertically slidably connected with sliding plates, the disc and the supporting ring are respectively rotationally connected to the two sliding plates, the reaction kettle is provided with a driving member for driving the two sliding plates to vertically move up and down, the two sliding plates are vertically provided with a communication groove, one end of the rotating shaft of the gear motor passes through one of the communication grooves, and one end of the stirring shaft passes through the other communication groove.

[0016] Preferably, the driving member comprises a lead screw, an inverted U-shaped fixed plate and a transmission rod coaxially arranged on the lead screw, the top ends of the two sliding plates are connected through the fixed plate, the lead screw is rotationally connected to the top end in the reaction kettle, and the bottom end of the lead screw passes through the fixed plate and is threadedly connected with the fixed plate, the transmission rod is arranged at the top end of the lead screw, and the top end of the transmission rod passes through the reaction kettle and is provided with a rotating disc outside the reaction kettle.

[0017] Preferably, a plurality of disturbance plates are arranged on each connecting plate along the length direction of the connecting plate.

[0018] Another object of the present application is to provide a use method of the production equipment of the o-tert-butyl phenol, the water level of the reaction liquid in the reaction kettle is located in the upper middle of one side of the disc, when in use, the isobutene gas is introduced into the dispersion pipe through the gas inlet pipe and is driven to rotate by the driving member, at this time, the isobutene gas is sprayed into the reaction liquid in the reaction kettle through each nozzle on the dispersion pipe to react, when the disc rotates, the disc drives each connecting plate to rotate along the rotation axis of the disc, at this time, because the water level of the reaction liquid is located in the upper middle of one side of the disc, part of the connecting plates on the disc are located outside the reaction liquid, and the remaining connecting plates are located in the reaction liquid, when the disc drives each connecting plate to rotate along the rotation axis of the disc, the side of the connecting plate provided with the groove located outside the reaction liquid will first contact the reaction liquid with the rotation of the disc, and then the connecting plate rotates into the reaction liquid with the rotation of the disc, at this time, when the isobutene gas overflows from the reaction liquid and floats in the reaction kettle, the isobutene gas floating in the reaction kettle can be brought into the reaction liquid again to participate in the reaction through the groove on the connecting plate located outside the reaction liquid following the rotation of the disc, and the reaction liquid in the reaction kettle can be stirred through each connecting plate on the disc.

[0019] After the reaction is completed, hot water is added into the reaction kettle through the hot water pipeline, the valve on the discharge pipe is opened after the hydrolysis is stirred, and then the reaction liquid can be discharged through the discharge pipe.

[0020] The beneficial effect of the present application is that the water level of the reaction liquid in the reaction kettle is located in the upper middle of one side of the disc, in use, the isobutene gas is introduced into the dispersion pipe through the gas inlet pipe and is driven to rotate by the driving member, at this time, the isobutene gas is sprayed into the reaction liquid in the reaction kettle through each nozzle on the dispersion pipe for reaction, when the disc rotates, the disc drives each connecting plate to rotate along the rotation axis of the disc, at this time, because the water level of the reaction liquid is located in the upper middle of one side of the disc, part of the connecting plates on the disc is located outside the reaction liquid, and the remaining connecting plates are located in the reaction liquid, when the disc drives each connecting plate to rotate along the rotation axis of the disc, the side of the connecting plate located outside the reaction liquid and provided with a groove is first contacted with the reaction liquid with the rotation of the disc, and then the connecting plate is rotated into the reaction liquid with the rotation of the disc, at this time, when the isobutene gas overflows from the reaction liquid and floats in the reaction kettle, the isobutene gas floating in the reaction kettle can be brought into the reaction liquid again to participate in the reaction through the groove on the connecting plate located outside the reaction liquid and rotating with the disc, and the reaction liquid in the reaction kettle can be stirred through each connecting plate on the disc.

[0021] After the reaction is completed, hot water is added into the reaction kettle through the hot water pipeline, the water is hydrolyzed after stirring, the valve on the discharge pipe is opened, and the hydrolyzed water is discharged through the discharge pipe, which is simple and convenient to use. BRIEF DESCRIPTION OF DRAWINGS

[0022] In order to more clearly illustrate the technical solutions in the embodiments of the present application or the prior art, the following will briefly introduce the drawings needed to be used in the embodiments or prior art description. Obviously, the drawings in the following description only some embodiments of the present application, and for those skilled in the art, other drawings can also be obtained without creative labor on the basis of these drawings.

[0023] Figure 1 It is a structural schematic diagram of the present embodiment;

[0024] Figure 2 It is a structural schematic diagram of the present embodiment for embodying the fixed plate;

[0025] Figure 3 It is a structural schematic diagram of the present embodiment for embodying the gas inlet pipe;

[0026] Figure 4 It is a structural schematic diagram of the present embodiment for embodying the connecting plate.

[0027] BRIEF DESCRIPTION OF DRAWINGS

[0028] In the figure: 1, reaction kettle; 2, disc; 3, air inlet pipe; 4, hot water pipeline; 5, dispersion pipe; 6, spray head; 7, connecting plate; 8, groove; 9, feed pipe; 10, discharge pipe; 12, inner gear ring; 13, circular groove; 14, motor; 15, gear; 16, support ring; 17, stirring shaft; 18, stirring rod; 19, sliding plate; 20, communication groove; 21, screw rod; 22, fixed plate; 23, transmission rod; 24, rotating disc; 25, disturbance plate. DETAILED DESCRIPTION

[0029] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the scope of protection of the present application.

[0030] Embodiment 1: A production device of o-tert-butyl phenol, as shown in Figure 1 and Figure 2 and Figure 3 , comprising a reaction kettle 1, a disc 2, and an air inlet pipe 3 and a hot water pipeline 4 arranged on the upper side of the outer wall of the reaction kettle 1, a dispersion pipe 5 horizontally arranged between the opposite sides of the reaction kettle 1, and a plurality of spray heads 6 arranged on the outer wall of the dispersion pipe 5, the air inlet pipe 3 being communicated with the dispersion pipe 5, the disc 2 being rotationally connected to one side in the reaction kettle 1, a plurality of connecting plates 7 being horizontally arranged on one side of the disc 2, and each of the connecting plates 7 being uniformly distributed along the circumference of the disc 2, a groove 8 for bringing isobutene gas into the reaction liquid in the reaction kettle 1 being arranged on one side of each of the connecting plates 7 along the length direction of the connecting plate 7, a driving member for driving the disc 2 to rotate being arranged on the reaction kettle 1, a feed pipe 9 being arranged on the top end of the reaction kettle 1, and a discharge pipe 10 with a valve being arranged on the bottom end of the reaction kettle 1.

[0031] as shown in Figure 1 and Figure 2 and Figure 3, the water level of the reaction liquid in the reaction kettle 1 is located in the middle and upper side of the disc 2, in use, the isobutene gas is introduced into the dispersion pipe 5 through the gas inlet pipe 3 and the disc 2 is driven to rotate by the driving member, at this time, the isobutene gas is sprayed into the reaction liquid in the reaction kettle 1 through each nozzle 6 on the dispersion pipe 5 to react, when the disc 2 rotates, the disc 2 drives each connecting plate 7 to rotate along the rotation axis of the disc 2, at this time, because the water level of the reaction liquid is located in the middle and upper side of the disc 2, part of the connecting plates 7 on the disc 2 is located outside the reaction liquid, and the remaining connecting plates 7 are located in the reaction liquid, when the disc 2 drives each connecting plate 7 to rotate along the rotation axis of the disc 2, the side of the connecting plate 7 located outside the reaction liquid, which is provided with a groove 8, will first contact the reaction liquid with the rotation of the disc 2, and then the connecting plate 7 will rotate into the reaction liquid with the rotation of the disc 2, at this time, when the isobutene gas overflows from the reaction liquid and floats in the reaction kettle 1, the isobutene gas floating in the reaction kettle 1 can be brought into the reaction liquid again to participate in the reaction through the groove 8 on the connecting plate 7 rotating with the disc 2 and located outside the reaction liquid, and the reaction liquid in the reaction kettle 1 can be stirred through each connecting plate 7 on the disc 2;

[0032] After the reaction is completed, hot water is added into the reaction kettle 1 through the hot water pipeline 4, and after the hydrolysis is stirred, the valve on the discharge pipe 10 is opened, and then the reaction liquid can be discharged through the discharge pipe 10, the outer wall of the reaction kettle 1 is provided with an electric heating plate (not shown in the figure), which is used to heat the reaction liquid in the reaction kettle 1, the reaction liquid enters the reaction kettle 1 through the feed pipe 9, and the use is simple and convenient

[0033] As Figure 2 The driving member includes an inner ring gear 12 and a circular groove 13 coaxially arranged on the disc 2, the inner ring gear 12 is coaxially located in the circular groove 13, and the outer wall of the inner ring gear 12 is fixedly connected with the groove wall of the circular groove 13, one side of the outer wall of the reaction kettle 1 is provided with a motor 14, and one end of the rotating shaft of the motor 14 penetrates through the kettle wall of the reaction kettle 1 and is provided with a gear 15, the gear 15 is located in the inner ring gear 12 and is engaged with the inner ring gear 12, the purpose of this setting is that when it is needed to drive the disc 2 to rotate, the motor 14 is only needed to be turned on, at this time, the rotating shaft of the motor 14 will drive the gear 15 to rotate, at this time, the gear 15 can drive the disc 2 to rotate through the inner ring gear 12 engaged therewith, and the use is simple and convenient.

[0034] As Figure 2 and Figure 4The inner wall of the reaction kettle 1 is rotatably connected with a support ring 16 opposite to the disc 2, and the end of each connecting plate 7 away from the disc 2 is fixedly connected with the support ring 16. When the disc 2 drives each connecting plate 7 to rotate along the rotation axis of the disc 2, the support ring 16 rotates with the disc 2 through each connecting plate 7. At this time, the support ring 16 can provide support force for the end of each connecting plate 7 away from the disc 2, reducing the bending of the connecting plate 7, and the use is simple and convenient.

[0035] As Figure 2 and Figure 3 The reaction kettle 1 is provided with a stirring part for stirring the reaction liquid in the reaction kettle 1. When the gear 15 rotates, the gear 15 drives the stirring part to stir the reaction liquid in the reaction kettle 1. The stirring part includes a stirring shaft 17 rotatably connected to one side of the inner wall of the reaction kettle 1. The stirring shaft 17 is horizontally arranged and opposite to the gear 15. At this time, one end of the stirring shaft 17 is located in the support ring 16. The end of the stirring shaft 17 close to the gear 15 is coaxially fixedly connected with the gear 15. The stirring shaft 17 is provided with a plurality of stirring rods 18. The dispersion pipe 5 is located below the disc 2 and the support ring 16 and is parallel to the stirring shaft 17. When the gear 15 rotates, the stirring shaft 17 rotates with the gear 15. At this time, the reaction liquid in the reaction kettle 1 can be further stirred by the stirring rods 18 on the stirring shaft 17. At this time, because the gear 15 drives the disc 2 to rotate through the inner gear ring 12 engaged with it, the rotation speed of the stirring shaft 17 is greater than that of the disc 2.

[0036] Because the dispersion pipe 5 is located below the disc 2 and the support ring 16 and is parallel to the stirring shaft 17, when the nozzle 6 on the dispersion pipe 5 sprays isobutene gas into the reaction liquid for reaction, the isobutene gas bubbles moving upward will enter between the disc 2 and the support ring 16. At this time, the reaction liquid in the reaction kettle 1 can be stirred by the stirring rods 18 on the stirring shaft 17, which facilitates the reaction of isobutene gas and reaction liquid, and the use is simple and convenient.

[0037] As Figure 2 and Figure 3The relative two sides of the inner wall of the reaction kettle 1 are vertically and slidably connected with sliding plates 19, the disc 2 and the supporting ring 16 are respectively rotationally connected on the two sliding plates 19, the reaction kettle 1 is provided with a driving part for driving the two sliding plates 19 to vertically move up and down, the two sliding plates 19 are vertically provided with communication grooves 20, one end of the rotating shaft of the motor 14 provided with the gear 15 passes through one of the communication grooves 20, one end of the stirring shaft 17 passes through the other communication groove 20, the gear 15 is located below the inner ring gear 12, the purpose of the setting is that the two sliding plates 19 are driven by the driving part to vertically move down, at this time, the supporting ring 16 and the disc 2 will respectively move down with the two sliding plates 19, at this time, because one end of the rotating shaft of the motor 14 provided with the gear 15 passes through one of the communication grooves 20, one end of the stirring shaft 17 passes through the other communication groove 20, so the positions of the gear 15 and the stirring shaft 17 in the reaction kettle 1 remain unchanged, with the vertical downward movement of the two sliding plates 19, the meshing state of the inner ring gear 12 on the disc 2 and the gear 15 will be disconnected, then the driving part continues to drive the two sliding plates 19 to vertically move down, and the motor 14 is turned off, until the gear 15 meshes with the inner ring gear 12 again, at this time, the gear 15 is located above the inner ring gear 12, then the motor 14 is turned on, at this time, the disc 2 can be driven to rotate again by the inner ring gear 12, at this time, the gear 15 and the inner ring gear 12 are disconnected and meshed again by the downward movement of the two sliding plates 19, the height position of the disc 2 and the supporting ring 16 in the reaction kettle 1 can be adjusted, the isobutene gas floating in the reaction kettle 1 can be brought into the reaction liquid, the disc 2 always rotates in one direction, and the top end of the disc 2 always locates outside the reaction liquid;

[0038] When the reaction of the isobutene gas and the reaction liquid is finished, the two sliding plates 19 can be vertically moved by the driving part, so that the meshing state of the inner ring gear 12 and the gear 15 is disconnected, after the meshing state of the inner ring gear 12 and the gear 15 is disconnected, the driving part stops working, at this time, the disc 2 will not be driven to rotate by the inner ring gear 12, but the gear 15 continues to drive the stirring shaft 17 to rotate to continue stirring the reaction liquid after the hot water is added by the stirring rods 18, at this time, the load of the motor 14 driving the gear 15 to rotate can be reduced, which is simple and convenient to use.

[0039] As Figure 2The driving member comprises a screw rod 21, an inverted U-shaped fixed plate 22, and a transmission rod 23 coaxially arranged on the screw rod 21. The top ends of the two sliding plates 19 are connected through the fixed plate 22. The screw rod 21 is rotationally connected to the top end in the reaction kettle 1. The bottom end of the screw rod 21 penetrates through the fixed plate 22 and is threadedly connected with the fixed plate 22. The transmission rod 23 is arranged at the top end of the screw rod 21. The top end of the transmission rod 23 penetrates through the reaction kettle 1 and is provided with a rotating disc 24 outside the reaction kettle 1. The purpose of the arrangement is that when the two sliding plates 19 need to be vertically moved, the rotating disc 24 only needs to be rotated. At this time, the rotating disc 24 drives the screw rod 21 to rotate through the transmission rod 23. At this time, because the bottom end of the screw rod 21 penetrates through the fixed plate 22 and is threadedly connected with the fixed plate 22, and the top ends of the two sliding plates 19 are connected through the fixed plate 22, when the screw rod 21 rotates, the fixed plate 22 can be pushed to vertically move the two sliding plates 19. The use is simple and convenient.

[0040] As Figure 2 and Figure 4 A plurality of disturbance plates 25 are arranged on each connecting plate 7 along the length direction of the connecting plate 7. When the disc 2 drives each connecting plate 7 to rotate along the rotation axis of the disc 2, the stirring effect of the connecting plate 7 on the reaction liquid can be increased through each disturbance plate 25 on each connecting plate 7. The use is simple and convenient.

[0041] In example 2, the reaction liquid in the reaction kettle 1 is located at the upper middle side of the disc 2. When the isobutene gas is introduced into the dispersion pipe 5 through the gas inlet pipe 3 and the disc 2 is driven to rotate by the driving member, the isobutene gas is sprayed into the reaction liquid in the reaction kettle 1 through each nozzle 6 on the dispersion pipe 5 to react. When the disc 2 rotates, the disc 2 drives each connecting plate 7 to rotate along the rotation axis of the disc 2. At this time, because the water level of the reaction liquid is located at the upper middle side of the disc 2, part of the connecting plates 7 on the disc 2 is located outside the reaction liquid, and the remaining connecting plates 7 are located inside the reaction liquid. When the disc 2 drives each connecting plate 7 to rotate along the rotation axis of the disc 2, one side of the connecting plate 7 located outside the reaction liquid, which is provided with the groove 8, is first in contact with the reaction liquid with the rotation of the disc 2, and then the connecting plate 7 rotates into the reaction liquid with the rotation of the disc 2. At this time, when the isobutene gas overflows from the reaction liquid and floats in the reaction kettle 1, the isobutene gas floating in the reaction kettle 1 can be brought into the reaction liquid again to participate in the reaction through the groove 8 on the connecting plate 7 located outside the reaction liquid and rotating with the disc 2. At the same time, the reaction liquid in the reaction kettle 1 can be stirred through each connecting plate 7 on the disc 2.

[0042] After the reaction is completed, hot water is added into the reaction kettle 1 through the hot water pipeline 4. After the hydrolysis is stirred, the valve on the discharge pipe 10 is opened, and the reaction liquid can be discharged through the discharge pipe 10.

[0043] Obviously, many modifications and variations of the present application are possible in light of the above teachings. It is, therefore, to be understood that within the scope of the appended claims and their equivalents, the application can be practiced otherwise than as specifically described.

Claims

1. A production apparatus for o-tert-butylphenol, characterized in that, The reactor includes a reactor (1), a disc (2), and an air inlet pipe (3) and a hot water pipeline (4) located above one side of the outer wall of the reactor (1). A dispersion pipe (5) is horizontally arranged below the opposite sides of the reactor (1), and several nozzles (6) are provided on the outer wall of the dispersion pipe (5). The air inlet pipe (3) is connected to the dispersion pipe (5). The disc (2) is rotatably connected to one side of the reactor (1). Several connecting plates (7) are horizontally arranged on one side of the disc (2), and each connecting plate (7) is evenly distributed along the circumference of the disc (2). Each connecting plate (7) has a groove (8) along the length of the connecting plate (7) for bringing isobutylene gas into the reaction liquid in the reactor (1). The reactor (1) is provided with a driving component for driving the disc (2) to rotate. The top of the reactor (1) is provided with a feed pipe (9), and the bottom of the reactor (1) is provided with a discharge pipe (10) with a valve. The driving component includes an internal gear ring (12) and a circular groove (13) coaxially opened on the disk (2). The internal gear ring (12) is coaxially located in the circular groove (13), and the outer wall of the internal gear ring (12) is fixedly connected to the groove wall of the circular groove (13). A motor (14) is provided on one side of the outer wall of the reactor (1), and one end of the rotating shaft of the motor (14) passes through the reactor wall of the reactor (1) and is provided with a gear (15). The gear (15) is located in the internal gear ring (12) and meshes with the internal gear ring (12).

2. The production equipment for o-tert-butylphenol as described in claim 1, characterized in that, The inner wall of the reactor (1) is rotatably connected to a support ring (16) opposite to the disk (2), and the end of each connecting plate (7) away from the disk (2) is fixedly connected to the support ring (16).

3. The production equipment for o-tert-butylphenol as described in claim 2, characterized in that, The reactor (1) is equipped with a stirring element for stirring the reaction liquid inside the reactor (1). When the gear (15) rotates, the gear (15) drives the stirring element to stir the reaction liquid inside the reactor (1).

4. The production equipment for o-tert-butylphenol as described in claim 3, characterized in that, The stirring component includes a stirring shaft (17) rotatably connected to one side of the inner wall of the reactor (1). The stirring shaft (17) is horizontally arranged and opposite to the gear (15). At this time, one end of the stirring shaft (17) is located inside the support ring (16). The end of the stirring shaft (17) close to the gear (15) is coaxially fixedly connected to the gear (15). Several stirring rods (18) are provided on the stirring shaft (17).

5. The production equipment for o-tert-butylphenol as described in claim 4, characterized in that, The dispersion tube (5) is located below the disc (2) and the support ring (16), and the dispersion tube (5) is parallel to the stirring shaft (17).

6. The production equipment for o-tert-butylphenol as described in claim 4, characterized in that, The inner walls of the reactor (1) are vertically slidably connected to sliding plates (19) on opposite sides. The disc (2) and the support ring (16) are rotatably connected to the two sliding plates (19). The reactor (1) is provided with a drive for driving the two sliding plates (19) to move vertically up and down. The two sliding plates (19) are vertically connected with connecting slots (20). One end of the rotating shaft of the motor (14) with gear (15) passes through one of the connecting slots (20), and one end of the stirring shaft (17) passes through the other connecting slot (20).

7. The production equipment for o-tert-butylphenol as described in claim 6, characterized in that, The driving component includes a lead screw (21), an inverted U-shaped fixed plate (22), and a transmission rod (23) coaxially mounted on the lead screw (21). The top ends of the two slide plates (19) are connected by the fixed plate (22). The lead screw (21) is rotatably connected to the top end inside the reactor (1), and the bottom end of the lead screw (21) passes through the fixed plate (22) and is threadedly connected to the fixed plate (22). The transmission rod (23) is located at the top end of the lead screw (21), and the top end of the transmission rod (23) passes through the reactor (1) and is provided with a turntable (24) located outside the reactor (1).

8. The production equipment for o-tert-butylphenol as described in claim 1, characterized in that, Each of the connecting plates (7) is provided with a few interfering moving plates (25) at intervals along the length direction of the connecting plate (7).

9. A method of using a production apparatus for o-tert-butylphenol according to any one of claims 1-8, characterized in that, The reaction liquid level in the reactor (1) is located in the upper middle part of one side of the disc (2). Isobutylene gas is introduced into the dispersion tube (5) through the gas inlet pipe (3) and the disc (2) is driven to rotate by the drive component. The isobutylene gas is sprayed into the reaction liquid in the reactor (1) through the nozzles (6) on the dispersion tube (5) to carry out the reaction. When the disc (2) rotates, the disc (2) drives the connecting plates (7) to rotate along the rotation axis of the disc (2). Because the reaction liquid level is located in the upper middle part of one side of the disc (2), some of the connecting plates (7) on the disc (2) are located outside the reaction liquid, and the remaining connecting plates (7) are located inside the reaction liquid. The disc (2) drives the connecting plates to rotate along the rotation axis of the disc (2). When the connecting plate (7) rotates along the rotation axis of the disk (2), the side of the connecting plate (7) with the groove (8) located outside the reaction liquid will first come into contact with the reaction liquid as the disk (2) rotates. Then the connecting plate (7) rotates into the reaction liquid as the disk (2) rotates. When the isobutylene gas overflows from the reaction liquid and floats in the reactor (1), it is brought into the reaction liquid again by the groove (8) on the connecting plate (7) that follows the rotation of the disk (2) and is located outside the reaction liquid. At the same time, the reaction liquid in the reactor (1) is stirred by the connecting plates (7) on the disk (2). After the reaction is complete, hot water is added to the reactor (1) through the hot water pipeline (4). After stirring and hydrolyzing, the valve on the discharge pipe (10) is opened and the contents are discharged through the discharge pipe (10).

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